Nickel-cobalt composite hydroxide and process for manufacturing same
US-2015364759-A1 · Dec 17, 2015 · US
US11380882B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11380882-B2 |
| Application number | US-201515517276-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 30, 2015 |
| Priority date | Oct 8, 2014 |
| Publication date | Jul 5, 2022 |
| Grant date | Jul 5, 2022 |
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A method for producing a M-carbonate precursor of a Li-M oxide cathode material in a continuous reactor, wherein M=NixMnyCozAn, A being a dopant, with x>0, y>0, 0≤z≤0.35, 0≤n≤0.02 and x+y+z+n=1, the method comprising the steps of: —providing a feed solution comprising Ni-, Mn-, Co- and A-ions, and having a molar metal content M″ feed, —providing an ionic solution comprising either one or both of a carbonate and a bicarbonate solution, the ionic solution further comprising either one or both of Na- and K-ions, —providing a slurry comprising seeds comprising M′-ions and having a molar metal content M′ seeds, wherein M′=Nix′Mny′Coz′A′n′, A′ being a dopant, with 0≤x′≤1, 0≤y′≤1, 0≤z′≤1, 0≤n′≤1 and x′+y′+z′+n′=1, and wherein the molar ratio M′ seeds/M″ feed is between 0.001 and 0.1, —mixing the feed solution, the ionic solution and the slurry in the reactor, thereby obtaining a reactive liquid mixture, —precipitating a carbonate onto the seeds in the reactive liquid mixture, thereby obtaining a reacted liquid mixture and the M-carbonate precursor, and —separating the M-carbonate precursor from the reacted liquid mixture.
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The invention claimed is: 1. A method for producing a M-carbonate precursor of a Li-M oxide cathode material in a continuous process in a reactor, wherein M=Ni x Mn y Co z A n , A being a dopant, with x>0, y>0, 0≤z≤0.35, 0≤n≤0.02 and x+y+z+n=1, the method comprising: introducing to the reactor a feed solution comprising Ni-, Mn-, Co- and A-ions, wherein the feed solution contains a total amount of Ni-, Mn-, Co- and A-ions £M″ feed ), introducing to the reactor an ionic solution comprising either one or both of a carbonate and a bicarbonate solution, the ionic solution further comprising either one or both of Na- and K-ions, pumping a slurry comprising seeds into the reactor, the seeds comprising M′-ions, wherein the slurry contains a total amount of M′ ions (M′ seeds ), wherein M′=Ni x′ Mn y′ Co z′ A′ n′ , A′ being a dopant, with 0≤x′≤1, 0≤y′≤1, 0≤z′≤1, 0≤n′≤1 and x′+y′+z′+n′=1, and wherein the molar ratio M′ seeds /M″ feed is between 0.001 and 0.04, mixing the feed solution, the ionic solution and the slurry in the reactor, thereby obtaining a reactive liquid mixture, precipitating a carbonate onto the seeds in the reactive liquid mixture, thereby obtaining a reacted liquid mixture and the M-carbonate precursor, and separating the M-carbonate precursor from the reacted liquid mixture. 2. The method according to claim 1 , wherein the seeds have a median particle size D50 between 0.1 and 3 μm. 3. The method according to claim 1 , wherein the M′-ions are present in a water insoluble compound that is selected from the group consisting of M′CO 3 , M′(OH) 2 , M′-oxide and MOOH. 4. The method according to claim 3 , wherein the water insoluble compound is either MnCO 3 or TiO 2 . 5. The method according to claim 1 , wherein the Ni-, Mn-, Co- and A-ions are present in a water soluble sulfate compound. 6. The method according to claim 1 , wherein a concentration of NH 3 in the reactor is less than 5.0 g/L. 7. The method according to claim 1 , wherein M=M′. 8. The method according to claim 1 , wherein the solid content in the slurry flow is between 30 and 300 g/L. 9. The method according to claim 1 , wherein the reactor is a continuous stirred tank reactor (CSTR). 10. The method according to claim 1 , further comprising the step of drying the separated M-carbonate precursor, wherein the dried M-carbonate precursor has a span defined as the value of (D90−D10)/D50 of its volumetric particle size distribution, and wherein the ratio M′ seeds /M″ feed is ≤0.01, such that a span<2 of the dried M-carbonate precursor is obtained. 11. A method for producing a lithium M-oxide cathode material for a rechargeable battery, comprising: providing a M-carbonate precursor by the method according to claim 1 , providing a Li precursor compound, mixing the M-carbonate and the Li precursor, and firing the mixture at a temperature between 600 and 1100° C. for at least 1 hr. 12. A method for producing a lithium M-oxide cathode material for a rechargeable battery, comprising: providing a M-carbonate precursor by the method according to claim 5 , providing a Li precursor compound, mixing the M-carbonate and the Li precursor, and firing the mixture at a temperature between 600 and 1100° C. for at least 1 hr. 13. A method for producing a lithium M-oxide cathode material for a rechargeable battery, comprising: providing a M-carbonate precursor by the method according to claim 3 , providing a Li precursor compound, mixing the M-carbonate and the Li precursor, and firing the mixture at a temperature between 600 and 1100° C. for at least 1 hr. 14. A method for producing a lithium M-oxide cathode material for a rechargeable battery, comprising: providing a M-carbonate precursor by the method according to claim 7 , providing a Li precursor compound, mixing the M-carbonate and the Li precursor, and firing the mixture at a temperature between 600 and 1100° C. for at least 1 hr. 15. A method for producing a lithium M-oxide cathode material for a rechargeable battery, comprising: providing a M-carbonate precursor by the method according to claim 10 , providing a Li precursor compound, mixing the M-carbonate and the Li precursor, and firing the mixture at a temperature between 600 and 1100° C. for at least 1 hr.
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